Converter primary dust removal system capable of reducing particulate matter emission and use method of converter primary dust removal system

A dust removal system and particle technology, applied in the field of converter dust removal, can solve the problems of increasing investment, operation management and operation maintenance costs, reducing the space occupied by the dehydrator, and failing to meet environmental protection requirements, etc., to achieve good fluid mechanics performance, Optimize group layout and reduce system resistance

Active Publication Date: 2021-11-09
NORTHEASTERN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0011] (2) By adding or extending the length of the existing gas and water separation device for dust removal, the cooling effect is improved, and the gas is effectively separated from the water; the invention patent with application number 201510180601.X discloses a dust removal method that improves the effect of wet dust removal System and method; by connecting more than one dedusting dehydration tank in series behind the pipeline fan of the wet dedusting system, and designing the structure inside the tank, the flue gas is compressed, sprayed, decelerated, swirled, folded flow, filter, and then reduce the concentration of dusty gas emissions to 30mg / Nm 3 The following; the utility model patent with application number 201320135423.5 discloses a gas and water separation device for converter wet dedusting; by prolonging the residence time of turbid circulating water in the dedusting equipment, the gas is effectively separated from the water, reducing the amount of gas emission, improve gas recovery rate; utility model patent application number 201820292564.0, announced a new OG dust removal system for converter flue gas; it uses ultra-clean dehydration dust collector to replace wet spin dehydrator, and ultra-clean dehydration dust removal The middle part of the device is replaced by a tube bundle, and the outer wall of the tube bundle is cooled by the external ambient air, which improves the cooling effect; however, the addition of a new gas and water separation device will increase the cost of investment, operation management and operation and maintenance, and prolong the existing dust removal. , The length of the water separation device needs to increase the space; at the same time, the dust concentration of the gas after dust removal is still only reduced to 30mg / Nm 3 , also unable to meet the current ≤20mg / Nm 3 environmental protection requirements;
[0012] (3) By adjusting the throat opening degree of the secondary flap venturi tube and the annular seam opening degree of the annular venturi tube, the airflow surge phenomenon of the new OG method is overcome; the utility model patent with the application number 201621409178.2 has published a A converter dust removal system, through the online monitoring device to detect the dust content in the flue gas, the control unit adjusts the speed of the fan according to the online dust content data, and automatically adjusts the throat opening degree of the secondary flap venturi tube, the ring seam venturi tube The opening of the ring seam ensures that the flue gas treated by the converter dust removal device meets the requirements of environmental protection; the invention patent application number is 201410285436. The water pipe and the curved swirl spray gun dehydrator reduce the space occupied by the dehydrator and meet the dehydration effect of the first dust removal; by adjusting the size of the throat ring seam of the secondary venturi tube, the problem that the fan speed cannot be operated at a low speed is solved, and the problem is overcome. The airflow surge phenomenon has been eliminated; the invention patent with the application number 201611254527.2 has announced a double closed-loop dynamic optimization OG method for converter gas recovery and fan energy-saving control method. The air pressure controls the speed of the fan, and through the organic combination of the two, the gas recovery and the energy-saving effect of the fan are guaranteed; however, in the above-mentioned published patents, adjusting the opening of the Venturi tube will increase the flow rate of dust and gas in the device, resulting in dust erosion on the inner wall of the device exacerbated and shortened system life

Method used

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  • Converter primary dust removal system capable of reducing particulate matter emission and use method of converter primary dust removal system
  • Converter primary dust removal system capable of reducing particulate matter emission and use method of converter primary dust removal system
  • Converter primary dust removal system capable of reducing particulate matter emission and use method of converter primary dust removal system

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0081] The structure of the primary dust removal system of the converter to reduce the emission of particulate matter is as follows: figure 1 As shown, it includes a converter 1, a primary spray scrubber 4, a secondary spray scrubber 7, an annular venturi tube 11, a flue gas water mist separator 15, a first cyclone dehydrator 17 and a second cyclone dehydrator 19;

[0082] The flue gas collection hood 2 cooperates with the converter 1, the flue gas collection hood 2 communicates with the top of the primary spray scrubber 4 through the vaporization cooling flue 3, the lower part of the primary spray scrubber 4 and the top of the secondary spray scrubber 7 pass through the system adjustment The pressure pipe 6 is connected, and the lower part of the secondary spray scrubber 7 is connected with the lower end of the annular venturi tube 11 through the first flue gas pipeline 9; , the circular seam venturi tube 11 and the dust removal pipeline 12 are connected through a 180° arc b...

Embodiment 2

[0113] The structure of the primary dedusting system of the converter for reducing particle emissions is the same as in Example 1, the difference is that:

[0114] (1) The first-stage conical blade swirl plate is composed of 4 blades, the second-stage conical-blade swirl plate is composed of 4 blades, and the third-stage conical-blade swirl plate is composed of 6 blades;

[0115] (2) The blade bending inclination angle of the first conical blade swirl plate is 7°; the blade bending inclination angle of the second conical blade swirl plate is 7°; the blade bending inclination angle of the third conical blade swirl plate is 9° ;

[0116] (3) The inside of the first-level spray scrubber is provided with 5 groups of dual-fluid aerosol spray guns, and each group of dual-fluid aerosol spray guns has 4 nozzles; There are 5 nozzles in the group-to-spray spiral spray gun;

[0117] (4) There are 3 air-water atomization spray guns in the first flue gas pipeline;

[0118] (5) There are...

Embodiment 3

[0130] The structure of the primary dedusting system of the converter for reducing particle emissions is the same as in Example 1, the difference is that:

[0131] (1) The first-stage conical blade swirl plate is composed of 5 blades, the second-stage conical-blade swirl plate is composed of 5 blades, and the third-stage conical-blade swirl plate is composed of 7 blades;

[0132] (2) The blade bending inclination angle of the first conical blade swirl plate is 9°; the blade bending inclination angle of the second conical blade swirl plate is 9°; the blade bending inclination angle of the third conical blade swirl plate is 10° ;

[0133] (3) The inside of the first-level spray scrubber is provided with 6 groups of dual-fluid aerosol spray guns, and each group of dual-fluid aerosol spray guns has 6 nozzles; There are 3 nozzles in the paired spray spiral spray gun;

[0134] (4) There are 4 air-water atomization spray guns in the first flue gas pipeline;

[0135] (5) There are ...

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Abstract

The invention discloses a converter primary dust removal system capable of reducing particulate matter emission and an using method of the converter primary dust removal system. According to the converter primary dust removal system, a flue gas collecting cover of the system is matched with a converter, and the flue gas collecting cover, a first-stage spray washing tower, a second-stage spray washing tower, a circular seam venturi tube, a flue gas and water mist separator, a first rotational flow dehydrator, a second rotational flow dehydrator and a primary dust removal fan sequentially communicate in series; the method comprises the steps that in the converter steelmaking process, the primary dust removal fan is started, converter flue gas is sequentially washed in the first-stage spray washing tower, the second-stage spray washing tower and the first flue gas pipeline, accelerated through the circular seam venturi tube and then injected with high-pressure steam to form water mist flue gas, the water mist flue gas enters the flue gas water mist separator, water flow formed by water drops under the rotational flow effect is separated from the flue gas, and the flue gas is dewatered by the first rotational flow dehydrator and the second rotational flow dehydrator and enters the primary dust removal fan. The method can ensure that the content of particulate matters in the flue gas reaches 15 mg / Nm <3> or below, and meets the emission requirements.

Description

technical field [0001] The invention relates to the technical field of converter dust removal treatment, in particular to a converter primary dust removal system for reducing particle emissions and a method for using the same. Background technique [0002] During the oxygen-blowing smelting process in the converter, the molten iron in the furnace reacts with oxygen to produce high-temperature flue gas up to 1600°C, which is called converter gas, and its main components are CO, CO 2 , SO 2 , N 2 , O 2 And iron-containing dust, which has the characteristics of high temperature, poisonous, flammable and explosive, and high dust content; in the middle stage of smelting, the CO content is as high as 80%, and the concentration of iron-containing dust reaches 150-200mg / Nm 3 , with high calorific value and large quantity, it is a valuable secondary energy source. Effective recovery and utilization of converter gas can not only greatly reduce the production cost of the steelmakin...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C21C5/40
CPCC21C5/40Y02P10/20
Inventor 朱苗勇刘志远蔡兆镇娄文涛姜嵇银
Owner NORTHEASTERN UNIV
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